JPH07116276B2 - Method for producing polyurethane resin - Google Patents
Method for producing polyurethane resinInfo
- Publication number
- JPH07116276B2 JPH07116276B2 JP62068764A JP6876487A JPH07116276B2 JP H07116276 B2 JPH07116276 B2 JP H07116276B2 JP 62068764 A JP62068764 A JP 62068764A JP 6876487 A JP6876487 A JP 6876487A JP H07116276 B2 JPH07116276 B2 JP H07116276B2
- Authority
- JP
- Japan
- Prior art keywords
- thf
- polyurethane resin
- copolyether
- polyol
- glycol
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4858—Polyethers containing oxyalkylene groups having more than four carbon atoms in the alkylene group
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polyurethanes Or Polyureas (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、ポリウレタン樹脂組成物に関する。TECHNICAL FIELD The present invention relates to a polyurethane resin composition.
(発明が解決しようとする問題点) ポリウレタン樹脂のソフトセグメント成分としてポリエ
ーテルがよく用いられる。中でもテトラヒドロフラン
(以下THFと称す)の重合体であるポリテトラメチレン
エーテルグリコールを用いたポリウレタン樹脂は弾性特
性、低温特性、耐加水分解性などの点において優れるた
め特に注目されている。(Problems to be Solved by the Invention) Polyether is often used as a soft segment component of polyurethane resin. Among them, a polyurethane resin using polytetramethylene ether glycol, which is a polymer of tetrahydrofuran (hereinafter referred to as THF), is particularly attractive because it is excellent in elastic properties, low temperature properties, hydrolysis resistance and the like.
しかし、ポリテトラメチレンエーテルグリコールはポリ
ウレタンに有用な分子量500〜4000のもので融点が20〜4
0℃の範囲にあり、常温或はそれ以下の温度では結晶化
が起こり、ハンドリング、作業性は勿論、常温で硬化を
必要とする塗料、コーテイング、シーリング等の分野に
おいて大きな問題となっている。従来、これらの分野で
は結晶化を防ぐため適当な有機溶剤を添加する方法が採
られているが、公害防止、合理性の観点から最近は非溶
剤系のものが指向され、ポリテトラメチレンエーテルグ
リコールの特性を所望しつつ、その結晶性の改善が強く
望まれている。However, polytetramethylene ether glycol has a molecular weight of 500 to 4000, which is useful for polyurethane, and has a melting point of 20 to 4
It is in the range of 0 ° C., and crystallization occurs at room temperature or lower temperature, which is a serious problem not only in handling and workability but also in the fields of coating, coating, sealing, etc., which require curing at room temperature. Conventionally, in these fields, a method of adding an appropriate organic solvent has been adopted in order to prevent crystallization, but recently, from the viewpoint of pollution prevention and rationality, a non-solvent system has been aimed at, and polytetramethylene ether glycol is used. It is strongly desired to improve the crystallinity while demanding the above characteristics.
ポリテトラメチレンエーテルグリコールの欠点を改良す
るためTHF/プロピレンオキシドコポリエーテルポリオー
ルが知られる[Journal of Polymer Science,58,857−8
63(1962)]。しかしこのポリオールはプロピレンオキ
シドとの共重合物であるためポリプロピレンオキシドポ
リオール同様、末端が2級水酸基であり、イソシアネー
ト基との反応性が低く、またポリウレタンの物性にも難
点をもち、結晶性は低く、常温で液状を保つものの満足
できるものではない。THF / propylene oxide copolyether polyols are known to improve the drawbacks of polytetramethylene ether glycol [Journal of Polymer Science, 58 , 857-8
63 (1962)]. However, since this polyol is a copolymer with propylene oxide, it has a secondary hydroxyl group at the end like polypropylene oxide polyol, its reactivity with isocyanate groups is low, and the physical properties of polyurethane are difficult, and its crystallinity is low. Although it remains liquid at room temperature, it is not satisfactory.
(問題点を解決するための手段) 本発明者らは上記実情に鑑み、鋭意検討した結果、THF
と3−アルキルTHFとをモル比85/15ないし20/80の混合
比で強酸触媒下に共重合反応して得られるコポリエーテ
ルポリオールは常温で液状を保ち、かつポリイソシアネ
ートとの反応性に富み、該ポリオールとポリイソシアネ
ート、鎖延長剤からなるポリウレタン樹脂はゴム弾性に
優れることを見出し、本発明に到達した。(Means for Solving Problems) The inventors of the present invention have made diligent studies in view of the above circumstances, and as a result, THF
Copolyether polyol obtained by copolymerization reaction of 3-alkyl THF with a molar ratio of 85/15 to 20/80 in the presence of a strong acid catalyst maintains a liquid state at room temperature and is highly reactive with polyisocyanate. The inventors have found that a polyurethane resin composed of the polyol, polyisocyanate, and chain extender has excellent rubber elasticity, and arrived at the present invention.
一般式: (式中R1、R2は一方が水素、もう一方がC1〜C4アルキル
基) で表わされる3−アルキル置換テトラヒドロフランの代
表例として3−メチルTHFをあげることができ、これは
米国特許第3,859,369号にCopelinにより記載された1,4
−ブテンジオールのヒドロホルミル化と水素添加によ
り、またイタコン酸の還元などにより合成される。THF
と3−メチルTHFとが共重合反応することは知られてい
る。本発明のコポリエーテルポリオールとはTHFと3−
メチルTHFとのモル混合比を85/15ないし20/80にとり、T
HFを開環しうる強酸、例えばクロロスルホン酸、フロロ
スルホン酸、過塩素産などにより通常0℃〜50℃の温度
で共重合して得られ、融点は10℃付近以下にあり、常温
では完全に液体状態を保持する。上記のモル混合比範囲
においてTHF/3−メチルTHF比を小さくとると融点は降下
する傾向を示し、従って融点は自由に変えられ、使用温
度、使用目的にあった融点をもつコポリエーテルを得る
ことができる。モル混合比20/80以下では実質的に融点
をもたないコポリエーテルとなるが、そのガラス転移点
が急に上昇するために、ポリウレタン樹脂の低温特性に
好ましくない。一方モル混合比85/15以上では融点の上
昇により結晶性が増し、目的に合わない。結晶性、ポリ
ウレタン樹脂物性とのバランスから好ましいコポリエー
テルポリオールを得るTHF/3−メチルTHFモル混合比は80
/20ないし30/70である。General formula: (In the formula, one of R 1 and R 2 is hydrogen and the other is a C 1 -C 4 alkyl group), 3-methyl THF can be mentioned as a representative example of a 3-alkyl-substituted tetrahydrofuran, which is described in US Pat. 1,4, described by Copelin in No. 3,859,369
-Synthesized by hydroformylation of butenediol and hydrogenation, reduction of itaconic acid and the like. THF
It is known that and 3-methyl THF undergo a copolymerization reaction. The copolyether polyol of the present invention means THF and 3-
The molar mixing ratio with methyl THF is 85/15 to 20/80, and T
Obtained by copolymerizing strong acids capable of ring-opening HF, such as chlorosulfonic acid, fluorosulfonic acid, and perchloric acid, usually at a temperature of 0 ° C to 50 ° C. Holds liquid state. When the THF / 3-methyl THF ratio is made small in the above molar mixing ratio range, the melting point tends to decrease, and therefore the melting point can be freely changed to obtain a copolyether having a melting temperature suitable for the use temperature and purpose. You can When the molar mixing ratio is 20/80 or less, it becomes a copolyether having substantially no melting point, but its glass transition point rises sharply, which is not preferable for the low temperature characteristics of the polyurethane resin. On the other hand, if the molar mixing ratio is 85/15 or more, the melting point rises and the crystallinity increases, which is not suitable for the purpose. From the balance of crystallinity and physical properties of polyurethane resin, a preferred copolyether polyol is obtained. The THF / 3-methyl THF molar mixing ratio is 80.
/ 20 to 30/70.
上記のコポリエーテルポリオールは常温で無色透明な液
体であるほか末端は一級水酸基であるためイソシアネー
ト基との反応性に富み、ポリプロピレンオキシドポリオ
ールやTHF/プロピレンオキシドコポリエーテルポリオー
ルの反応性の約3ないし4倍である。従ってポリウレタ
ン樹脂の分野でも常温硬化プロセス、更に反応射出成型
(RIM)プロセスなどに好適である。The above-mentioned copolyether polyol is a colorless transparent liquid at room temperature and has a primary hydroxyl group at the end, so it is highly reactive with isocyanate groups, and the reactivity of polypropylene oxide polyol and THF / propylene oxide copolyether polyol is about 3 to 4 Double. Therefore, even in the field of polyurethane resin, it is suitable for a room temperature curing process and further a reaction injection molding (RIM) process.
本発明で使用するコポリエーテルポリオールの分子量
は、特に限定はなく、目的とするポリウレタン樹脂によ
って広範に使用でき、500ないし5000であるが、特に800
ないし4500のものが本発明の効果を発揮する。The molecular weight of the copolyether polyol used in the present invention is not particularly limited, can be widely used depending on the target polyurethane resin, and is 500 to 5,000, but particularly 800
Nos. 4 to 4500 exhibit the effects of the present invention.
一方、ポリイソシアネート化合物とは、分子内にイソシ
アネート基を2個以上有するもので、例えばトリレンジ
イソシアネート(TDI)、4,4′−ジフェニルメタンジイ
ソシアネート(MDI)、ヘキサメチレンジイソシアネー
ト、キシリレンジイソシアネート、イソホロンジイソシ
アネート、ナフチレンジイソシアネート、水添ジフェニ
ルメタンジイソシアネート等一般的にポリウレタン樹脂
の合成に用いられるポリイソシアネート化合物があげら
れ、これらは単独または二種以上混合して用いられる。On the other hand, the polyisocyanate compound is a compound having two or more isocyanate groups in the molecule, for example, tolylene diisocyanate (TDI), 4,4'-diphenylmethane diisocyanate (MDI), hexamethylene diisocyanate, xylylene diisocyanate, isophorone diisocyanate. Examples thereof include polyisocyanate compounds generally used in the synthesis of polyurethane resins such as naphthylene diisocyanate and hydrogenated diphenylmethane diisocyanate, and these may be used alone or in combination of two or more.
鎖延長剤は、通常この種のポリウレタン製造に使用され
るプレポリマーの末端イソシアネート基と反応する活性
水素原子含有化合物であって、これを具体的に示すと、
2以上の水酸基、アミノ基をもつ化合物で、エチレング
リコール、プロピレングリコール、1,4−ブタンジオー
ル、1,6−ヘキサンジオール、キシリレングリコール、
グリセリン、トリメチロールプロパン、エチレンジアミ
ン、プロピレンジアミン、フェニレンジアミン、ジアミ
ノジフェニルメタン、メチレン・ビス(2−クロロアニ
リン)等である。他にヒドラジン化合物、水等もあげる
ことができる。ジアミン、ヒドラジン、水を用いて得ら
れる樹脂はポリウレタン−ウレアである。The chain extender is an active hydrogen atom-containing compound that reacts with a terminal isocyanate group of a prepolymer usually used in the production of polyurethanes of this type, and when it is specifically shown,
Compounds with two or more hydroxyl groups and amino groups, such as ethylene glycol, propylene glycol, 1,4-butanediol, 1,6-hexanediol, xylylene glycol,
Glycerin, trimethylolpropane, ethylenediamine, propylenediamine, phenylenediamine, diaminodiphenylmethane, methylene bis (2-chloroaniline) and the like. Other examples include hydrazine compounds and water. The resin obtained using diamine, hydrazine and water is polyurethane-urea.
本発明のポリウレタン樹脂組成物は、例えばコポリエー
テルポリオール化合物とポリイソシアネート化合物とを
反応させてイソシアネート基含有の前駆体(プレポリマ
ー)を合成し、その後、鎖延長剤を反応させることによ
り、即ち二段法によっても得られるし、またコポリエー
テルポリオール、ポリイソシアネート、鎖延長剤を同時
に反応させるワンショット法など通常のポリウレタン樹
脂の製法で得られる。The polyurethane resin composition of the present invention comprises, for example, reacting a copolyether polyol compound with a polyisocyanate compound to synthesize an isocyanate group-containing precursor (prepolymer), and then reacting with a chain extender, It can also be obtained by a step method, or by a usual polyurethane resin production method such as a one-shot method in which a copolyether polyol, a polyisocyanate and a chain extender are simultaneously reacted.
上記の合成において反応温度はプロセス、用途等によっ
て変わってくるが、一般的には50〜200℃範囲で行われ
るが、本発明の場合、コポリエーテルポリオールの融点
が低いために50℃以下の温度でも反応が可能である。一
方各成分の組成比は目的とするポリウレタン樹脂によっ
て変わるが、プレポリマーはイソシアネート基を含有す
る必要があり、コポリエーテルポリオール化合物の水酸
基1当量に対しポリイソシアネート化合物のイソシアネ
ート基が1以上、好ましくは1,2以上にとられる。最終
反応物の配合比はいずれの方法でもイソシアネート基1
当量に対しコポリエーテルポリオールと鎖延長化合物の
全活性水素原子当量が0.9〜1.1にとられる。In the above synthesis, the reaction temperature varies depending on the process, application, etc., but is generally carried out in the range of 50 to 200 ° C., but in the case of the present invention, the temperature is 50 ° C. or lower because the melting point of the copolyether polyol is low. But the reaction is possible. On the other hand, the composition ratio of each component varies depending on the target polyurethane resin, but the prepolymer needs to contain an isocyanate group, and the isocyanate group of the polyisocyanate compound is 1 or more per 1 equivalent of the hydroxyl group of the copolyether polyol compound, preferably Taken over 1,2. The compounding ratio of the final reaction product is 1 for the isocyanate group in any method.
The total active hydrogen atom equivalents of the copolyether polyol and the chain extension compound are taken to be 0.9 to 1.1 with respect to the equivalent amount.
上記の反応において必要に応じ、触媒、安定剤等を添加
することができる。触媒としては例えばトリエチルアミ
ン、トリブチルアミン、ジブチル錫ジラウレート、オク
チル酸第一錫等があり、安定剤としては例えばアイオノ
ール(BHT)、ジステアリルチオジプロピオネート、ジ
・ベータナフチルフェニレンジアミン、トリ(ジノニル
フェニル)フォスファイト等があげられる。In the above reaction, a catalyst, a stabilizer and the like can be added if necessary. Examples of the catalyst include triethylamine, tributylamine, dibutyltin dilaurate and stannous octoate, and examples of the stabilizer include ionol (BHT), distearyl thiodipropionate, di-betanaphthylphenylenediamine, tri (dinonyl). Phenyl) phosphite and the like.
本発明のポリウレタン樹脂は、常温液状のポリプロピレ
ンオキシドポリオール、THF/プロピレンオキシドコポリ
エーテルポリオールから得られるポリウレタン樹脂の物
性よりかなり優れ、ポリテトラメチレンエーテルポリオ
ールより得られるポリウレタン樹脂の物性と殆んど変ら
ない優れた弾性体である。The polyurethane resin of the present invention is considerably superior to the physical properties of the polyurethane resin obtained from polypropylene oxide polyol and THF / propylene oxide copolyether polyol which are liquid at room temperature, and is almost the same as the physical properties of the polyurethane resin obtained from polytetramethylene ether polyol. It is an excellent elastic body.
(実施例) 次に本発明を実施例によって更に詳しく説明する。実施
例中コポリエーテルポリオールの水酸基価(OH価 mg K
OH/g)はピリジン−無水酢酸法で求めこれより数平均分
子量を求めた。3−メチルTHFユニット、THFユニットの
組成分析、末端水酸基解析は13C−NMR(日本電子製FX−
60)、融点(Tm)およびガラス転移点(Tg)はDSC(理
学電機製DSC−8230)によったポリウレタン物性はJIS−
K6301に順じて測定した。(Example) Next, the present invention will be described in more detail with reference to Examples. The hydroxyl value of the copolyether polyol in the examples (OH value mg K
OH / g) was determined by the pyridine-acetic anhydride method, and the number average molecular weight was determined from this. Composition analysis of 3-methyl THF unit, THF unit, and terminal hydroxyl group analysis are performed by 13 C-NMR (JEOL FX-
60), melting point (Tm) and glass transition point (Tg) are based on DSC (Rigaku Denki DSC-8230)
The measurement was performed according to K6301.
実施例1 脱水されたTHF288.4g(4モル)、3−メチルTHF86.1g
(1モル)[モル混合比80/20]を撹拌機、温度計、N2
シール装置を備えた1四ツ口セパラブルフラスコに仕
込み、温度10℃で70%過塩素酸10.5g、無水酢酸95gを添
加、8時間重合反応を行った。反応終了液を20%水酸化
ナトリウム水溶液500gで中和し、以下一般的方法に順
じ、モノマー回収、加水分解、精製操作を行い、常温で
無色透明な液体であるコポリエーテルグリコール275g
(収率73.4%)を得た。このものは水酸基価103.9、数
平均分子量1080、NMR解析の結果、末端は一級水酸基の
みであり、THFコニットと3−メチルTHFユニットとのモ
ル組成比は86/14のコポリエーテルグリコールであっ
た。DSC解析の結果、Tm=1℃、Tg=−85℃であった。Example 1 288.4 g (4 mol) of dehydrated THF and 86.1 g of 3-methyl THF
(1 mol) [molar mixing ratio 80/20] with a stirrer, thermometer, N 2
The flask was placed in a 1-necked separable flask equipped with a sealing device, and 10.5 g of 70% perchloric acid and 95 g of acetic anhydride were added at a temperature of 10 ° C. to carry out a polymerization reaction for 8 hours. Neutralize the reaction completed liquid with 500 g of 20% sodium hydroxide aqueous solution, follow the general method below to perform monomer recovery, hydrolysis and purification operations, and copolyether glycol 275 g which is a colorless transparent liquid at room temperature.
(Yield 73.4%) was obtained. As a result of NMR analysis, this product had a hydroxyl value of 103.9, a number average molecular weight of 1080, and was found to have only primary hydroxyl groups at the end, and it was a copolyether glycol having a molar composition ratio of THF conit and 3-methyl THF unit of 86/14. As a result of DSC analysis, Tm = 1 ° C. and Tg = −85 ° C.
更に撹拌機、温度計、N2シール−減圧装置を備えた500c
c四ツ口セパラバルフラスコに上記コポリエーテルグリ
コール100gをとり、100℃で1時間真空乾燥を行い、こ
れを充分脱水したジメチルアセトアミド100gに溶解混合
し、蒸留精製した4,4′−ジフェニルメタンジイソシア
ネート(MDI)を用い、公知の方法[J.poly.sci.chem.E
ds.,13,1657('75)]にて30℃における反応速度定数K1
(kg/eg・sec)を求めたところ、K1=4.3×10-3が得ら
れ、同時に測定したTHF−プロピレンオキシドコポリエ
ーテルグリコール(分子量980、K=1.2×10-3)、ポリ
プロピレンオキシドグリコール(分子量1000、K1=0.9
×10-3)に比べ約4倍であった。500c equipped with stirrer, thermometer, N 2 seal-pressure reduction device
c 100 g of the above-mentioned copolyether glycol was placed in a four-neck separaval flask, vacuum dried at 100 ° C. for 1 hour, dissolved and mixed in 100 g of sufficiently dehydrated dimethylacetamide, and distilled and purified to obtain 4,4′-diphenylmethane diisocyanate ( Known method [J.poly.sci.chem.E]
ds., 13,1657 ('75)] reaction rate constant K 1 at 30 ℃
When Kg / eg · sec was calculated, K 1 = 4.3 × 10 −3 was obtained, and THF-propylene oxide copolyether glycol (molecular weight 980, K = 1.2 × 10 −3 ) and polypropylene oxide glycol were measured at the same time. (Molecular weight 1000, K 1 = 0.9
X10 -3 ) was about 4 times.
次に同様な500ccセパラブルフラスコに上記コポリエー
テルグリコール200gをとり、100℃で1時間真空乾燥を
行い、MDI106gを添加、60℃で5時間反応させてプレポ
リマー(NCO=6.50%)を得た。この150gを別に用意し
た混合器にとり、脱気後1,4−ブタンジオール10gを添
加、数分間に充分混合後、予熱した20cm×30cm×0.2cm
ガラスモールドに注ぎ、110℃のオーブン中で16時間キ
ュアリングを行い、ポリウレタンシートを得た。これを
20℃の恒温室にて1週間放置し、物性測定に供した。プ
レポリマー、ポリウレタンの物性を表−1に示した。Next, 200 g of the above copolyether glycol was placed in a similar 500 cc separable flask, vacuum dried at 100 ° C. for 1 hour, 106 g of MDI was added, and reacted at 60 ° C. for 5 hours to obtain a prepolymer (NCO = 6.50%). . Take 150 g of this in a mixer prepared separately, add 10 g of 1,4-butanediol after degassing, mix thoroughly for a few minutes, then preheat 20 cm × 30 cm × 0.2 cm
It was poured into a glass mold and cured in an oven at 110 ° C for 16 hours to obtain a polyurethane sheet. this
The sample was left to stand in a thermostatic chamber at 20 ° C for 1 week and subjected to physical property measurement. The physical properties of the prepolymer and polyurethane are shown in Table-1.
実施例2〜4および比較例1、2 THFと3−メチルTHFとのモル混合比を50/50(実施例
2)、30/70(実施例3)、90/10(比較例1)、10/90
(比較例2)、80/20(分子量2000、実施例4)に設定
し、過塩酸/無水酢酸の量を目的分子量に合うように変
化させる以外は実施例1と同様にして得たコポリエーテ
ルグリコール、ポリウレタンの物性を表−1に示した。Examples 2-4 and Comparative Examples 1, 2 The molar mixing ratio of THF and 3-methyl THF was 50/50 (Example 2), 30/70 (Example 3), 90/10 (Comparative Example 1), 10/90
(Comparative Example 2), Copolyether obtained in the same manner as in Example 1 except that the ratio was set to 80/20 (molecular weight 2000, Example 4) and the amount of perchloric acid / acetic anhydride was changed to match the target molecular weight. Physical properties of glycol and polyurethane are shown in Table-1.
比較例3、4 市販のポリテトラメチレンエーテルグリコール(PTG、
分子量1020)、公知の方法で得たTHF/プロピレンオキシ
ド(30重量%)コポリエーテルグリコール(PPTG、分子
量980)、および実施例1と同様にして得たポリウレタ
ンの物性を表−1に示した。Comparative Examples 3 and 4 Commercially available polytetramethylene ether glycol (PTG,
Table 1 shows the molecular weight of 1020), THF / propylene oxide (30% by weight) copolyether glycol (PPTG, molecular weight of 980) obtained by a known method, and the physical properties of the polyurethane obtained in the same manner as in Example 1.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 渡辺 治生 神奈川県横浜市鶴見区大黒町7番43号 保 土谷化学工業株式会社中央研究所鶴見分室 内 (72)発明者 竹内 修一 神奈川県横浜市鶴見区大黒町7番43号 保 土谷化学工業株式会社中央研究所鶴見分室 内 (56)参考文献 特開 昭57−202320(JP,A) ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Haruo Watanabe 7-43, Oguro-cho, Tsurumi-ku, Yokohama-shi, Kanagawa Hodogaya Chemical Industry Co., Ltd. Central Research Laboratory Tsurumi Branch Office (72) Inventor Shuichi Takeuchi Yokohama-shi, Kanagawa 7-43, Daikoku-cho, Tsurumi-ku, Tsurumi Branch, Central Research Laboratory, Hodogaya Chemical Co., Ltd. (56) Reference JP-A-57-202320 (JP, A)
Claims (1)
ヒドロフランとのモル比85/15ないし20/80の混合比でこ
れらを共重合させて得られたコポリエーテルポリオー
ル、ポリイソシアネート化合物および鎖延長剤を反応さ
せることを特徴とするポリウレタン樹脂の製造方法。1. Reacting a copolyether polyol, a polyisocyanate compound and a chain extender obtained by copolymerizing tetrahydrofuran and 3-alkyltetrahydrofuran at a molar ratio of 85/15 to 20/80. A method for producing a polyurethane resin, comprising:
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62068764A JPH07116276B2 (en) | 1987-03-25 | 1987-03-25 | Method for producing polyurethane resin |
| DE8888302323T DE3877231T2 (en) | 1987-03-25 | 1988-03-17 | COMPOSITION OF POLYURETHANE RESIN. |
| EP88302323A EP0284289B1 (en) | 1987-03-25 | 1988-03-17 | Polyurethane resin composition |
| US07/172,574 US4960849A (en) | 1987-03-25 | 1988-03-24 | Polyurethane from a copolyether of tetrahydrofuran and 3-alkyl tetrahydrofuran |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62068764A JPH07116276B2 (en) | 1987-03-25 | 1987-03-25 | Method for producing polyurethane resin |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4310016A Division JP2678547B2 (en) | 1992-11-19 | 1992-11-19 | Polyurethane resin |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63235320A JPS63235320A (en) | 1988-09-30 |
| JPH07116276B2 true JPH07116276B2 (en) | 1995-12-13 |
Family
ID=13383128
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62068764A Expired - Lifetime JPH07116276B2 (en) | 1987-03-25 | 1987-03-25 | Method for producing polyurethane resin |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US4960849A (en) |
| EP (1) | EP0284289B1 (en) |
| JP (1) | JPH07116276B2 (en) |
| DE (1) | DE3877231T2 (en) |
Families Citing this family (37)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5354837A (en) * | 1992-12-22 | 1994-10-11 | Hodogaya Chemical Co., Ltd. | Low-temperature liquid urethane prepolymer |
| JPH07268050A (en) * | 1994-03-31 | 1995-10-17 | Nippon Polyurethane Ind Co Ltd | Method for producing fast-curing spray elastomer |
| KR100239204B1 (en) * | 1995-06-23 | 2000-01-15 | 야마모토 카즈모토 | Polyurethane Elastic Fiber and Manufacturing Method thereof |
| JPH10279573A (en) * | 1997-04-02 | 1998-10-20 | Mitsubishi Gas Chem Co Inc | Method for producing 3-methyltetrahydrofuran |
| US7101955B1 (en) | 1998-11-12 | 2006-09-05 | Alliant Techsystems Inc. | Synthesis of energetic thermoplastic elastomers containing both polyoxirane and polyoxetane blocks |
| US6815522B1 (en) | 1998-11-12 | 2004-11-09 | Alliant Techsystems Inc. | Synthesis of energetic thermoplastic elastomers containing oligomeric urethane linkages |
| EP1144473B1 (en) * | 1998-11-12 | 2003-09-24 | Alliant Techsystems Inc. | Synthesis of energetic thermoplastic elastomers containing both polyoxirane and polyoxetane blocks |
| US6997997B1 (en) | 1998-11-12 | 2006-02-14 | Alliant Techsystems Inc. | Method for the synthesis of energetic thermoplastic elastomers in non-halogenated solvents |
| US6989431B2 (en) * | 2003-05-09 | 2006-01-24 | Acushnet Company | Golf balls comprising chiral diols or chiral cyclic ethers |
| US6949617B2 (en) * | 2003-05-09 | 2005-09-27 | Acushnet Company | Golf balls comprising chiral diols or chiral cyclic ethers |
| US7105628B2 (en) | 2002-08-27 | 2006-09-12 | Acushnet Company | Compositions for golf equipment |
| US6780964B2 (en) | 2001-08-30 | 2004-08-24 | Hodogaya Chemical Co., Ltd. | Method for preparing polyether polyol copolymer |
| US7098274B2 (en) | 2002-08-27 | 2006-08-29 | Acushnet Company | Compositions for golf equipment |
| US7014574B2 (en) * | 2002-07-15 | 2006-03-21 | Acushnet Company | Compositions for golf balls |
| US7138477B2 (en) | 2002-08-27 | 2006-11-21 | Acushnet Company | Compositions for golf equipment |
| US7105623B2 (en) | 2002-08-27 | 2006-09-12 | Acushnet Company | Compositions for golf equipment |
| US7138476B2 (en) | 2002-08-27 | 2006-11-21 | Acushnet Company | Compositions for golf equipment |
| US7115703B2 (en) | 2002-08-27 | 2006-10-03 | Acushnet Company | Compositions for golf equipment |
| US7378483B2 (en) | 2002-08-27 | 2008-05-27 | Acushnet Company | Compositions for golf equipment |
| US7101951B2 (en) | 2002-08-27 | 2006-09-05 | Acushnet Company | Compositions for golf equipment |
| US7138475B2 (en) | 2002-08-27 | 2006-11-21 | Acushnet Company | Compositions for golf equipment |
| US7157545B2 (en) | 2002-08-27 | 2007-01-02 | Acushnet Company | Compositions for golf equipment |
| US20060014918A1 (en) * | 2003-05-09 | 2006-01-19 | Acushnet Company | Compositions for use in golf balls |
| US7265195B2 (en) | 2004-06-02 | 2007-09-04 | Acushnet Company | Compositions for golf equipment |
| US7256249B2 (en) | 2004-06-02 | 2007-08-14 | Acushnet Company | Compositions for golf equipment |
| US7253242B2 (en) | 2004-06-02 | 2007-08-07 | Acushnet Company | Compositions for golf equipment |
| US7276570B2 (en) | 2004-06-02 | 2007-10-02 | Acushnet Company | Compositions for golf equipment |
| US7253245B2 (en) | 2004-06-02 | 2007-08-07 | Acushnet Company | Compositions for golf equipment |
| EP1803755B1 (en) | 2004-10-20 | 2013-08-14 | Asahi Glass Company, Limited | Urethane resin solution, process for its production and process for producing urethane resin |
| CN101039981B (en) * | 2004-10-21 | 2010-09-08 | 旭硝子株式会社 | Polyurethane resin and method for producing polyurethane resin solution |
| JP4455662B2 (en) * | 2006-11-27 | 2010-04-21 | タツタ電線株式会社 | Optical drop cable for protection |
| JP5436190B2 (en) * | 2009-12-17 | 2014-03-05 | 三菱電機株式会社 | Elevator rope |
| JP5797697B2 (en) * | 2012-07-30 | 2015-10-21 | 三洋化成工業株式会社 | Polyurethane resin |
| WO2014057057A1 (en) * | 2012-10-10 | 2014-04-17 | Basf Se | Catching device made of thermoplastic polyurethane |
| TWI768017B (en) | 2017-05-30 | 2022-06-21 | 日商保土谷化學工業股份有限公司 | Process for producing bio-based polyether polyol, bio-based polyether polyol and bio-based polyurethane resin |
| JP7166854B2 (en) | 2017-09-27 | 2022-11-08 | キヤノン株式会社 | Electrophotographic member, process cartridge and electrophotographic apparatus |
| CN115785385B (en) * | 2022-12-09 | 2024-09-06 | 江苏华大新材料有限公司 | High-transmittance non-yellowing polyurethane resin for curved-surface-screen mobile phone and preparation method and application thereof |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3358042A (en) * | 1963-09-20 | 1967-12-12 | Quaker Oats Co | Process for recovering polytetramethylene ether glycol |
| JPS4825438B1 (en) * | 1969-03-03 | 1973-07-28 | ||
| FR2134765A5 (en) * | 1971-04-20 | 1972-12-08 | France Etat | |
| US3726905A (en) * | 1971-07-01 | 1973-04-10 | Du Pont | Conversion of butanediol to tetrahydrofuran in the presence of tall oil |
| US3859369A (en) * | 1971-07-26 | 1975-01-07 | Du Pont | Process for the production of 2-methyl-1,4-butanediol |
| US3941849A (en) * | 1972-07-07 | 1976-03-02 | The General Tire & Rubber Company | Polyethers and method for making the same |
| US4120850A (en) * | 1977-09-06 | 1978-10-17 | E. I. Du Pont De Nemours And Company | Polyether urethane polymers prepared from a copolymer of tetrahydrofuran and ethylene oxide |
| DE2801129A1 (en) * | 1978-01-12 | 1979-07-19 | Bayer Ag | MODIFIED POLYISOCYANATE HAVING SULPHIC ACID ESTER GROUPS |
| US4235751A (en) * | 1979-04-30 | 1980-11-25 | E. I. Du Pont De Nemours And Company | Modified montmorillonite clay catalyst |
| JPS57202320A (en) * | 1981-06-05 | 1982-12-11 | Japan Synthetic Rubber Co Ltd | Preparation of polyether glycol |
| JPS58189221A (en) * | 1982-04-28 | 1983-11-04 | Dai Ichi Kogyo Seiyaku Co Ltd | Production of polyurethane resin |
| AT374816B (en) * | 1982-07-27 | 1984-06-12 | Vianova Kunstharz Ag | METHOD FOR PRODUCING WATER-DETERMINATABLE BINDERS CARRYING OXAZOLIDING GROUPS |
| US4590285A (en) * | 1983-06-08 | 1986-05-20 | E. I. Du Pont De Nemours And Company | Process for preparing a mixture of tetrahydrofuran and 3-alkyl tetrahydrofuran and copolymers thereof |
| DE3346136A1 (en) * | 1983-12-21 | 1985-07-04 | Basf Ag, 6700 Ludwigshafen | METHOD FOR THE CONTINUOUS PRODUCTION OF POLYOXIBUTYLENE POLYOXIALKYLENE GLYCOLES |
| US4739027A (en) * | 1985-12-17 | 1988-04-19 | Westinghouse Electric Corp. | Resilient polyurethane elastomer |
-
1987
- 1987-03-25 JP JP62068764A patent/JPH07116276B2/en not_active Expired - Lifetime
-
1988
- 1988-03-17 DE DE8888302323T patent/DE3877231T2/en not_active Expired - Lifetime
- 1988-03-17 EP EP88302323A patent/EP0284289B1/en not_active Expired - Lifetime
- 1988-03-24 US US07/172,574 patent/US4960849A/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63235320A (en) | 1988-09-30 |
| EP0284289A2 (en) | 1988-09-28 |
| DE3877231T2 (en) | 1993-05-06 |
| EP0284289B1 (en) | 1993-01-07 |
| US4960849A (en) | 1990-10-02 |
| EP0284289A3 (en) | 1990-01-10 |
| DE3877231D1 (en) | 1993-02-18 |
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